Running the Process Model

Congratulations on completing the flowsheet and entering the process model conditions. Now you are ready to put your model to the test. Example 4-3, the cracking reaction, can now be simulated.

Once you've clicked OK to run the process model, the Control Panel window will appear. This window gives you a look at the ASPEN PLUS^TM "thinking process." Phrases indicating the PFR block is being executed will scroll across the screen. When the simulation is complete, the Control Panel will read: Simulation calculations completed.

Interpreting the Results

1. Once the simulation is complete, click the Next button on the Control Panel.

2. A window will pop up with three choices. Mark the first choice, Display Run-Status results form, and click ok.

3. A window titled Results Summary will appear. Click on Streams in the navigation window on the left.

For the Example 4-3 simulation the stream results screen should look like this:

Note that, down the left side of the screen, are the different parameters: temperature, pressure, mole flow, etc. Along the top row are the stream id names, in this case 1 and 2 (inlet and product). This forms a grid of information that can be interpreted easily.

In Example 4-3, the problem asks for the PFR volume that will achieve an 80% conversion. As you recall, when entering the process model conditions, you guessed a volume by entering an arbitrary length and diameter of the PFR. In order to complete the problem, you must see what conversion your process model obtained. Recall that conversion is defined as:

To solve for conversion, do the following with the results:

1. Under Mole Flow for ethane, calculate the moles of ethane that reacted: stream 1 - stream 2

2. Divide this number by the molar flowrate of ethane into the PFR: stream 1.

If you followed the example exactly, using a length of 10 feet and a diameter of 3 feet, you should get a conversion of 76%.

The dimensions of the PFR did not achieve an 80% conversion. Therefore, you need to go back and adjust them. It is easiest to vary the length of the PFR while holding the diameter constant. In this example, since the conversion was too low, you must INCREASE the length of the PFR.

Changing Process Conditions and Rerunning the Model

Adjusting the input conditions is very straightforward, just follow these steps:

1. With the mouse pointer, click on the close button for the Results window and then the Control Paenl window (do not close ASPEN PLUS™)
   

2. You should now see the input specifications window (where you entered information on reaction kinetics, reactor size, etc...)

3. Browse to the Blocks > B1 > Setup page from the left explorer window and click on the Configuration tab.

4. Click in the box of the value you wish to change. In this case change the Length to a value greater than 10 feet (Hint: Try 11.42 feet!).

5. Use the explorer window on the left to browse through the input data if you need to change more parameters. If not, keep clicking Next until you are prompted with "Run Simulation Now?"

6. Rerun the simulation, and check your results.

In Example 4-3, you will find that a length of 11.42 feet and a diameter of 3 feet will achieve an 80% conversion. To finish the problem, the volume of a PFR with these dimensions is V = 80.72 ft³.

1. Introduction

2. Accessing ASPEN PLUS^TM

3. Creating a Reaction Engineering Process Model
   1. Building a Process Flowsheet
   2. Entering Process Conditions
4. Running the Process Model
   1. Interpreting the Results
   2. Changing Process Conditions and Rerunning the Model
5. Example Problems
   1. 8-5: Adiabatic Production of Acetic Anhydride
   2. 8-5: Operation of a PFR with Heat Exchanger
6. Other Need-to-Knows
   1. Saving your Process Model
   2. Printing your Process Model
   3. Changing Names of Streams and Unit Operations
   4. Changing Units of Parameters
   5. Exiting ASPEN PLUS^TM
7. Credits

Back to ASPEN PLUS^TM Main Page